Application of Louis I. Hansen and Alexis G. Coutsicos

332 F.2d 825, 51 C.C.P.A. 1447
CourtCourt of Customs and Patent Appeals
DecidedJune 11, 1964
DocketPatent Appeal 7108
StatusPublished
Cited by1 cases

This text of 332 F.2d 825 (Application of Louis I. Hansen and Alexis G. Coutsicos) is published on Counsel Stack Legal Research, covering Court of Customs and Patent Appeals primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

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Application of Louis I. Hansen and Alexis G. Coutsicos, 332 F.2d 825, 51 C.C.P.A. 1447 (ccpa 1964).

Opinion

SMITH, Judge.

Appellants have appealed from a decision of the Board of Appeals, adhered To on reconsideration, affirming the primary examiner’s rejection of claims, numbered 19-25, 27-32 and 37-39, of appellants’ application, Serial No. 670,-386, filed July 8, 1957, entitled “Epoxidation Process.” The grounds of rejection are that the claims 1) relate to an obvious invention and hence are unpatentable over the prior art (35 U.S.C. § 103), and 2) failed to define properly the invention (as required by 35 U.S.C. § 112) in that they are unduly broad and indefinite.

Epoxidation, to which the invention relates, is a method by which -¿=C-groups of certain mono or poly non-conjugated ethylenically unsaturated compounds are converted to oxirane or epoxy groups, -C - C-, by oxidation in \ / O acidic medium. Conventionally, peracetic or performie acids are used as oxidizing agents, such acids being formed in situ by reacting hydrogen peroxide, H2O2, with either acetic or formic acid. As stated in the DuPont Bulletin, of record infra:

“Hydrogen peroxide, which is a mild oxidizing agent, often must be transformed into an organic peracid or activited by some other means to make full use of its oxidizing powgj» # # #
“The method operates best under conditions for in situ formation of an organic peracid, contributing to a highly efficient and economical reaction. By the in situ formation of peracid is meant a one-step reaction in which peracid is formed and used in the presence of the material to be epoxidized.
* * * -X* * *
“Mixing hydrogen peroxide and an organic acid such as glacial acetic acid results in an equilibrium mixture of peracetic acid, hydrogen peroxide, water, and acetic acid.

H2O2 + ch3co2h - v ch3co3h + H20

“In the absence of a strong acid catalyst, the attainment of equilibri *826 um is impractically slow, especially at temperatures up to 40 °C. * * * ” [Emphasis added.]

Appellants point out that concentrated sulfuric acid is conventionally used as “strong acid catalyst”, the specification noting, however, that certain defects reside in employing either peracetic or performic acid alone with or without catalyst.

Appellants’ invention is employing as an epoxidizing composition a “synergistic mixture of short chain organic acids as propionic or acetic in combination with formic in the presence of an oxidizing agent [hydrogen peroxide], with or without an acid catalyst.”

Appellants’ epoxidizable compounds are described as mono or poly non-conjugated unsaturated, substituted and unsubstituted, straight and branched chain, aliphatic and cycloaliphatic compounds of at least 5 carbon atoms which may have the general basic formula set forth. Other groups of ethylenically unsaturated compounds are also indicated. The specification points out that the disclosed “mixed acetic acid and formic acid epoxidation process * * * operates most successfully commercially with long chain unsaturated compounds such as fatty acids, their esters, nitrites and amides” and that epoxidizable “compounds particularly representative of those indicated herein are unsaturated glycerides, acids, and simple or complex esters derived from vegetable, animal, marine and petroleum sources.” A list of typical epoxidizable compounds containing ethylenic groups is set forth.

According to the application, the epoxidizing composition may contain hydrogen peroxide in an amount of about 0.3 to 5 moles per mole of epoxidizable ethylenic unsaturation and the workable range of the mixed short chain organic acids is approximately 0.1 to 0.6 moles acetic acid, and from approximately 0.1 up to about 0.5 moles formic acid per mole of unsaturation. The acid catalyst is preferably sulfuric acid, which may be utilized as 0.25% to 5% concentrated acid based on the total weight of the combined short chain acid and formic-acid, or a cationic exchange resin may be employed as the catalyst in amounts varying up to 50% based on the weight of the material treated.

The epoxidation reaction is exothermic and the preferred procedure is to charge all unsaturated material to the reactor, add the epoxidizing materials over a period of time, heat to a temperature of 120° F. to 140° F., maintain the temperature at 132° F. to 138° F., and then recover the oily product. “The reaction times and temperature are related to the physical and chemical properties of the compounds to be epoxidized” and the “overall rate of reaction is a function of the concentration of the reactants.” Inert solvents may be employed.

The application indicates that the combined use of a short chain acid (as acetic acid) with formic acid is superior to the use of either acid alone with respect to oxirane and iodine values and other characteristics.

The epoxidized compounds are useful as chemical intermediates, in the textile-industry, in the formation of plastics, as-plasticizers for vinyl resins and nitrocellulose, in printing inks, in alkyd resins, and in many other uses known to the-art.

There are sixteen claims on appeal. All involve a method for producing a compound containing an oxirane linkage, which comprises the steps of mixing an. epoxidizable ethylenic compound selected from the group defined in the claims, with an epoxidizing composition of reactants comprising hydrogen peroxide and a mixture of short chain monocarboxylic acids from 1 through 3 carbon atoms (Claim 29), effecting epoxidation,. and separating the product containing an oxirane linkage. In claims 19 to 25, 27, 28, 30 and 31, the acids in the epoxidizing composition are acetic and formic; while claims 32 and 28 call for a cationic resin as the catalyst, and claim 39 calls for sulfuric acid as the catalyst. The-specified proportions, times and temperatures are recited in claims 23 to 25, 27 to 32, and 37 to 39. The use of an. *827 inert organic solvent is recited in claims .21, 22 and 28.

All of the appealed claims are the so-called “Jepson” type claims in which the specific improvement is defined, after .general recitals, as

“ * * * the steps comprising mixing the said unsaturated epoxidizable compound with an epoxidizing composition of reactants comprising in combination acetic acid, formic acid and hydrogen peroxide, effecting an epoxidation of said ethylenic group by said epoxidizing •composition, and separating from the mixture a reacted product containing an oxirane linkage, (el. 19)” [Emphasis added.]

No useful purpose will be served in 'full reproduction of the claims in this -opinion. They stand rejected on the two separate grounds above referred to. The rejection under 35 U.S.C. § 103 is based ■on the following prior art:

Niederhauser et al., 2,485,160, October 18, 1949

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332 F.2d 825, 51 C.C.P.A. 1447, Counsel Stack Legal Research, https://law.counselstack.com/opinion/application-of-louis-i-hansen-and-alexis-g-coutsicos-ccpa-1964.